Apparatus and Method for Surface Treatment of a Food Product

ABSTRACT

A method and apparatus for treatment of an outer surface of a food product are provided using a fluid having properties selected for treating the surface and bringing the fluid into contact with an outer surface of the food product in a generally continuous manner in a commercial food processing environment.

FIELD

A method and apparatus for treating the surface of a food product, andin particular a method and apparatus of treating the surface of a foodproduct by contacting the surface of the food product with a fluidhaving properties selected for treating the surface.

BACKGROUND

A continual objective in the food processing industry is to preventunacceptably high levels of microbial activity on the food productsthemselves and on devices for processing the food products that contactthe food products. Another objective is to reduce costs associated withthe processing of food products. Costs can be reduced by increasingproductivity, including both increasing the rate at which food isprocessed and reducing any periodic down time necessary for cleaning.

Steam pasteurization has been used to heat the surface of food products,such as meat, to treat the surface in a non continuous manner where apiece of meat is stopped in a steam region and steam is directed at themeat while stopped. For example, U.S. Pat. No. 6,291,003 discloses anapparatus having three regions separated by doors, a dewatering region,a steam region, and a coolant region. A controller controls a conveyorto move meat between the three regions, including stopping the conveyerin the steam region for the application of steam.

A problem with typical steam treatment methods and devices is that thesteam tends to form condensate on the outer surfaces of the foodproduct. The condensate is formed rapidly as the high temperature steamfirst contacts the much lower temperature food product. Once acondensate layer forms on the outer surface of a food product, thecondensate acts as a barrier to additional heat transfer from hightemperature steam. Thus, when steam condenses to form condensate on anouter surface of a food product, the effectiveness of the continuedsteam treatment is significantly lowered.

SUMMARY

A method and apparatus for treating an outer surface of a food producthaving generally consistent cross-sectional geometry are provided. Themethods include placing a food product on an advancement mechanism. Asleeve is provided for generating a flow of fluid, such as steam, havingselected properties to treat the outer surface of the food product. Thefood product is passed in a feed direction through the steam sleeveusing the advancement mechanism. While the food product is passingthrough the steam sleeve, a flow of steam is generated therearound. Thesteam contacts the outer surface of the food product to elevate thesurface temperature to levels high enough for microbial reduction.

Internal passageways or channels may be formed in an interior of thesleeve and sized approximately with the same shape and dimension of afood product that is being treated. The internal dimensions of thesleeve may be sized such that there is a generally constantcross-sectional area and shape between the inlets and outlets. A sleevemay have one or more helical channels or planar channels that channel afluid, such as steam, at a consistent high velocity along the outersurface of the food product surface as the product is advanced throughthe sleeve. Fluid inlets and outlets are placed at the end of thechannels and may extend through the sleeve walls.

Applying steam to the product advantageously can achieve an extremelyrapid thermal surface pasteurization of the food product. The steaminherently provides high heat transfer rates, and when steam is appliedat high velocities, increased rates of heat transfer may be achieved.

The arrangement of the channel or channels within the steam sleeve maybe configured to maximize heat transfer from the steam to the foodproduct which provides the benefits of reducing the necessary exposuretime of the food product in the steam sleeve, thereby increasingmanufacturing efficiency and the speed at which the food product may beadvanced through the steam sleeve. Another benefit is a reduction of thesleeve length. By reducing the sleeve length, production space for foodprocessing can be saved and the sleeve can be added to existingprocessing equipment with minimal modifications.

Another benefit is that focusing the heat treatment on the surface mayminimize any adverse impact on texture, flavor or other properties ofthe food product. Yet another benefit of the steam sleeve is that it mayminimize the amount of post-treatment cooling required to return theproduct to the original thermal state.

A benefit of having the helical or generally planar steam channels isthat the flow velocity generates centrifugal forces that can tend tokeep moving the steam condensate to the outer part of the channel andaway from the surface of the food product. If the condensate were notmoved away from the surface, it could act as an insulating barrier onthe product surface, slowing the heat transfer.

Using multiple helical channels solves a problem encountered in tryingto maintain high velocities in a longer single helix. As the steamtravels along the helix it slows due to the volume reduction that occursdue to steam condensation, which increases further from the inlet.Another advantage of using multiple helical channels is that themultiple channels may accommodate opposing flow in sequential channelsto ensure adequate coverage of the outer surfaces of the food product bythe fluid.

The overall length of the sleeve can determine the desired number ofhelical channels or planar channels. For instance, a single helicalchannel may be provided in a shorter sleeve or a double helix may beprovided in a longer sleeve. The longer the sleeve, the more helicalchannels may be needed to maintain high velocities of steam.

The methods may further include the step of circulating the flow ofsteam within a channel having an inlet for introduction of the steaminto the sleeve and an outlet for removal of the steam and condensatefrom the sleeve after circulation. In addition, the method may includeproviding a condensate removal mechanism positioned adjacent the sleeveand in fluid communication therewith for removing excess condensate.

The steam sleeve may include multiple interconnected spiral or helicalchannels, allowing the steam to be introduced into the inlet of thechannel and follow the helical channel around the outer surface of thefood product to treat the outer surface of the food product. Themultiple interconnected helical channels may be arranged such that theinlet and the outlet are positioned so that the flow of steam is in ageneral direction along or opposite to that of the feed direction of thefood product.

More than one set of interconnected helical channels may be provided,such that each has its own inlet for the introduction of steam into thesleeve and its own outlet for removal of the steam and condensate fromthe sleeve. Where multiple interconnected helical channels are provided,one of the channels may have the inlet and outlet positioned so that theflow of steam is in a general direction opposite to that of the feeddirection of the food product and another may have the inlet and outletpositioned so that the flow of steam is in the same general direction asthat of the feed direction of the food product. In this manner, thesteam will flow in one channel in the direction of the feed and in theother channel opposite to the direction of the feed to ensure adequateand balanced coverage of the surface with steam. In addition, thecirculation rates of the steam within the sleeve at opposite endsthereof can be generally the same to further ensure consistent steamtreatment throughout the sleeve.

When a longer steam sleeve is desired, more than one set ofinterconnected helical channels may be used, and each of the helicalchannels may be multidirectional. Each of the helical channels may havepair of fluid inlets and at least one outlet. The pair of fluid inletsmay be positioned proximate the mid section of the sleeve. As the fluidis introduced into the pair of fluid inlets, one of the inlets may causethe fluid to flow in the helical channel toward the entrance opening ofthe sleeve and the other one of the inlets may cause the fluid to flowin the same helical channel toward the exit opening of the sleeve.

The step of passing the food product, such as elongated food product orlog of food, in the feed direction through the steam sleeve using theadvancement mechanism may include the step of forming a general sealbetween the outer surface of the food product and the steam sleeve usinga generally flexible wiper element. The wiper element may be positionedat both the entrance and the exit of the steam sleeve and may be sizedto have an opening slightly smaller than the profile of the food productand positioned to ensure that minimal steam escapes the steam sleeve.The step of passing the food product in a feed direction through thesteam sleeve using the advancement mechanism and generating the flow ofsteam in a steam sleeve while the food product is passing therethroughmay occur generally simultaneously in a continuous manner.

The step of circulating the flow of steam in a steam sleeve within achannel having an inlet for introduction of steam into sleeve and anoutlet for removal of the steam from the sleeve may include the step offorming multiple channels each having its own inlet and outlet. Each ofthe multiple channels may be substantially planar, therefore defining afluid path of about one revolution around the interior of the sleeve.

The food product is preferably advanced in a feed direction through thesteam sleeve at a predetermined rate.

The method may include the step of selecting the predetermined rate andthe fluid properties to achieve a satisfactory microbial reduction onthe surface of the food product.

The apparatus for use in the above methods and other methods comprises asteam sleeve having an entrance opening and an exit opening. Theentrance and exit openings of the steam sleeve are sized approximatelythe same as the profile of the food product in order to accommodate thefood product therein. A plurality of grooves or channels are formed onan interior of the steam sleeve between the entrance opening and theexit opening. The channels direct the flow of fluid at least partiallyaround an outer portion of the food product and at least one of thechannels has a fluid inlet and at least one of the channels has a fluidoutlet to permit introduction and removal of the fluid into the steamsleeve.

At least two of the plurality of channels may be connected to permit theflow of fluid therebetween. The plurality of channels may be connectedin a generally spiral or helical arrangement. The channels may also beconnected to internal piping within the sleeve to facilitate fluid flowbetween the channels.

A seal element may be provided proximate at least one of the entranceand exit openings of the sleeve. The seal element has an openingsubstantially the same size of the profile of the food product. Theopening of the seal element also may be smaller than the opening of atleast one of the entrance and exit openings of the steam sleeve. Theseal element is configured to provide a seal between the steam sleeveand the food product to inhibit the fluid from escaping to maintaindesired flow characteristics of the fluid, and to maintain the fluid atan elevated temperature.

The fluid may comprise steam having a predetermined properties selectedto treat the outer surface of the food product, such as for preventingunacceptable levels of microbial activity. Other treatment fluids oranti-microbial fluids may be used, or may be combined with the steam.High velocity steam may be used in the steam sleeve to treat the outersurface of the food product. High velocity steam can be advantageousbecause it can have a relatively high heat transfer rate and thus cancause a greater reduction in microbial activity on the surface of thefood product.

The entrance and exit openings of the steam sleeve may be shaped similarto the cross-sectional shape of the food product. For example, theopenings may be generally circular-shaped for generally circular foodproducts. Other opening shapes include square and rectangular in orderto accommodate, respectively, square and rectangular food products.Alternatively, the entrance and exit openings of the steam sleeve may begenerally D-shaped for different types of food product having agenerally D-shaped profile. With some product shapes, such as someD-shaped products, there can be a greater variance in the profile of thefood product. Thus, the D-shaped steam sleeve may be sized toaccommodate variations in the profiles of food product. In order to forma seal between the steam sleeve and the food product in order to reducesteam from escaping, to maintain desirable flow characteristics of thesteam within the sleeve, and to maintain a higher temperatures of thesteam within the steam sleeve, a wiper material may be provided aroundthe opening and exit of the D-shaped steam sleeve.

A different steam sleeve configuration may comprise a plurality ofplates that are sandwiched together. Each of the plates may have achannel formed therein. Sandwiched between the plates may be dividers,which may comprise the wipers, in order to keep the steam fromtransferring from one channel to another in the steam-sleeve. Each ofthe channels can have its own inlet and outlet. When multiple channelsand plates are arranged in a sandwiched fashion, it is preferable thatthe flow alternates. For example, in one channel flow may be clockwiseand in an adjacent channel, counterclockwise.

The sleeve may be used as part of a commercial food processingoperation. The commercial food processing operation may proceed throughmultiple treatment areas where the food product is subjected to varioustreatments, such as a cooking zone, a water deluge zone, a watersubmergence zone, a chilling zone, an equilibration zone, and a slicingzone. The sleeve may be used during any part of the treatment cycle, andin particular may be used prior to an equilibration zone and a slicingzone to reduce microbial activity on the surface of the food product.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a perspective view of a steam sleeve according to a firstembodiment having multiple steam flow channels and generally D-shapedopenings;

FIG. 2 is a side elevation view of the steam sleeve of FIG. 1 with afood product being advanced therethrough via an advancement mechanism;

FIG. 3 is a section view taken along line 3-3 of FIG. 2;

FIG. 4 is a section view taken along line 4-4 of FIG. 2;

FIG. 5A is a perspective view of a pusher device of the advancementmechanism;

FIG. 5B is a sectional side elevation view of the pusher device of FIG.5A;

FIG. 6 is a diagrammatic flow chart depicting a product treatment cycle;

FIG. 7 is a perspective view of a steam sleeve according to a secondembodiment having multiple helical flow channels;

FIG. 8 is a side elevation schematic view of the steam sleeve of FIG. 7showing multiple helical flow channels;

FIG. 9 is a side elevation sectional view of the steam sleeve of FIG. 8;

FIG. 10 is a section view taken along line 10-10 of FIG. 9;

FIG. 11 is a section view taken along line 11-11 of FIG. 9;

FIG. 12 is a section view taken along line 12-12 of FIG. 9;

FIG. 13 is a section view taken along line 13-13 of FIG. 9;

FIG. 14 is a perspective view of a steam sleeve according to a thirdembodiment having multiple helical flow channel;

FIG. 15 is a side elevation section view of the steam sleeve of FIG. 14;

FIG. 16 is a section view taken along line 16-16 of FIG. 15;

FIG. 17 is a section view taken along line 17-17 of FIG. 15;

FIG. 18 is a plot showing a predicted thermal model of the temperatureat various depths from the surface of the food product compared totravel time through the steam sleeve; and

FIG. 19 is a diagrammatic side elevation view of the steam sleeve ofFIG. 14 positioned for use with a slicing mechanism.

DETAILED DESCRIPTION OF THE DRAWINGS

A method and apparatus for treating the surface of a food product 5 areprovided using a fluid having properties for treating the surface of thefood product and bringing the fluid into contact with an outer surfaceof the food product 5 in a generally continuous manner in a commercialfood processing environment.

As illustrated in FIGS. 1-19, a treatment sleeve 10, 100 or 200 isprovided having an entrance opening and an exit opening. Positionedbetween the entrance opening and the exit opening of the treatmentsleeve 10, 100 or 200 and in an interior thereof are a plurality ofchannels 16, 110 and 120 or 210 and 211. The channels 16, 110 and 120 or210 and 211 and the entrance opening and exit opening are configuredsuch that when a food product 5 is being passed-through the treatmentsleeve 10, 100 or 200 the outer surface of the food product 5 is exposedto the channels 16, 110 and 120 or 210 and 211. Treatment fluid iscirculated through the channels 16, 110 and 120 or 210 and 211, thuscoming into contact and treating the outer surface of the food product5.

The fluid used within the treatment sleeve 10, 100 or 200 is preferablysteam. The steam is supplied to the channels 16, 110 and 120 or 210 and211 for circulation via inlets and outlets for the channels. The steamis preferably delivered with desired properties, such as saturated at aparticular pressure or at a predetermined temperature, into the channels16, 110 and 120 or 210 and 211 effective to treat the outer surface ofthe food product by facilitating heat transfer from the steam to theouter surface of the food product 5.

As the steam contacts the outer surface of the food product 5, some ofthe steam may condense and impart a large amount of heat to the productsurface, but also form a layer of insulating condensate. The condensatehas a lower heat transfer rate as compared to the condensing steam. Toremove condensate from contact with the outer surface of the foodproduct 5, the steam is preferably circulated through the channels 16,110 and 120 or 210 and 211 with a generally predetermined velocity tocreate sufficient circumferential forces to draw the condensate awayfrom the outer surface of the food product 5 and toward walls of thechannels 16, 110 and 120 or 210 and 211.

The channels 16, 110 and 120 or 210 and 211 define flow paths for thesteam. The flow path is preferably of a length selected to limit theamount of pressure drop and/or velocity reduction of the steam to ensuresufficient heat transfer from the steam to the outer surface of the foodproduct 5 during treatment. In one embodiment, illustrated in FIGS. 1-4,each generally planar channel 16 makes generally about one revolutionaround the interior of the treatment sleeve and thus has a generallyshort flow path. In another embodiment, illustrated in FIGS. 14-18, apair of helical flow channels 210 and 211 revolve multiple times aroundthe interior of the treatment sleeve 200 while advancing from the exitopening to the entrance opening of the sleeve 200, thus having a longerflow path than the flow path of FIGS. 1-4. In yet another embodiment,illustrated in FIGS. 7-13, two helical channels 110 and 124 are formedaround the interior of the treatment sleeve 100. The treatment sleeve100 of FIGS. 7-13 is longer than the treatment sleeve of FIGS. 14-18.However, the use of multidirectional flow within each of the helicalchannels 110 and 120, as will be discussed in greater detail below andas opposed to the unidirectional helical flow channels 210 and 211,reduces the overall flow channel lengths 110 and 120 to minimize theamount of pressure drop/velocity reduction of the steam to ensuresufficient heat transfer from the steam to the outer surface of the foodproduct 5 to treat the outer surface.

One or more wiper elements 14 and 220 are provided either in theinterior of the treatment sleeve 10 or adjacent the entrance and/or exitopenings of the treatment sleeve 10 and 200. The wiper elements 14 and220 have an opening therethrough that is sized smaller than the entranceor exit opening of the treatment sleeve 10 and 200. In one aspect, theopening of the wiper element 14 and 220 may be sized smaller than aprofile of the food product 5. As the food product 5 is advanced throughthe interior of the treatment sleeve 10 and 200, the portion of thewiper 14 and 220 adjacent the wiper opening is in contact, or close tobeing in contact, with the outer surface of the food product 5. Thewiper 14 and 220 is preferably made of a flexible material and functionsto maintain the steam within the treatment sleeve 10 and 200, maintaindesired flow characteristics and prevent unnecessary decreases in thetemperature within the treatment sleeve 10 and 200, and, if in contactwith the outer surface of the food product 5, to wipe away any excesscondensate on the surface of the food product 5.

The food product 5 is advanced through the treatment sleeve 10, 100 or200 while the steam is circulating through the one or more channels 16,110 and 120 or 210 and 211 in a generally continuous operation. Byadvancing the food product 5 through the treatment sleeve 10, 100 or 200in a generally continuous operation, food processing efficiency can beimproved compared to systems where a food product is advancedintermittently through a sealed steam chamber having doors or otherbarriers that must be opened and closed with each steam cycle.

The length of the treatment sleeve 10, 100 and 200 and the advancementrate of the food product 5 combine to provide a dwell time, the amountof time the food product is in contact with the steam in the treatmentsleeve. The dwell time and the heat transfer rate due to the steamapplied to the outer surface of the food product 5 combine to determinethe amount of heat transferred from the steam to the food product 5while the food product 5 is advancing through the treatment sleeve 10,100 and 200.

The steam transfers heat to the food product 5 and by conductionpermeates the food product 5 to various depths, depending upon the dwelltime and the heat transfer rate due to the steam. A one second dwelltime, as illustrated in the predicted thermal model of FIG. 18, resultsin elevated temperatures on the surface and very close to the surfacesufficient to treat the surface, while not permeating very deeply intothe food product 5. Thus, the majority of the food product 5, which ispositioned inwardly from the outer surface of the food product 5, is notsubject to substantially elevated temperatures. This contributes tominimal changes in the texture and appearance of the food product 5 ascompared to a food product not advanced through the treatment sleeve 10,100 or 200. In addition, not substantially elevating the temperature ofthe food product 5 inwardly of the surface thereof results in arelatively fast cool time for the product 5 to return to its originalthermal state after leaving the treatment sleeve 10, 100 or 200. Thedwell time within the sleeve, and the temperature of the fluid, arepreferably selected to allow for optimized slicing of the food productwhen used upstream of a slicing station. For example, if the foodproduct is raised to too high of a temperature and at too deep of adepth, slicing can be difficult, and tearing of the food product mayresult. Tearing can be undesirable in certain applications where theaesthetic appearance of the sliced food product is adversely affected.

As illustrated in FIG. 18, the temperature on the surface of the foodproduct 5 is predicted to be between about 150° F. and 200° F. after aone to three second dwell time within the sleeve as the product has beenadvanced therethrough. Moving inwardly within the food product 5 fromthe surface thereof about 0.005 inches, the temperature is predicted tobe between about 150° F. and about 200° F. Moving further inward toabout 0.017 inches, the temperature is predicted to be between about 75°F. and about 125° F. Even further inward of the outer surface of thefood product 5 to about 0.033 inches, the temperature is predicted to bebetween about 25° F. and about 75° F. Thus, the temperature on the outersurface of the food product 5 is highest, and then the temperaturerapidly decreases the further inward from the outer surface of the foodproduct 5.

Turning now to more of the details of the various aspects of thetreatment sleeves 10, 100 and 200, the sleeve 10 illustrated in FIGS.1-4 has generally D-shaped entrance and exit openings, while the sleeves100 and 200 illustrated in FIGS. 7-17 have generally circular entranceand exit openings. Other openings, such as rectangular and square, mayalso be used, depending upon the profile of the food product.

The openings of the treatment sleeves 10, 100, and 200 are configuredbased on the profile of the food product 5 for which it is associated.For example, meat products comprising bologna and sausage are generallycircular shaped in profile and consistently have similar sized profiles.Due to the relatively consistent sizing of the circular-profiled foodproducts 5, the size of the treatment sleeve 100 and 200 entrance andexit openings is sized sightly larger than the size of the food productprofile. Other meat products, such as ham, are allowed to naturallysettle in their casings, resulting in a generally D-shaped profile,having a flattened bottom. Due to the natural settling, there can bevariances in the size of the resulting D-shaped profiles. To accommodatethe variances in food product profiles, the D-shaped openings are sizedless closely to the product profiles than the generally circularopenings. To further accommodate various sizes of D-shaped openings, thecorresponding wiper elements 14 are larger in size. Therefore, whenthere is a smaller D-shaped food product 5 advancing through thetreatment sleeve 10, the wiper 14 contacts or closely contacts the outersurface thereof. When a relatively larger D-shaped food product 5 isadvancing through the treatment sleeve 10, the wiper 14 flexes toaccommodate the size while still contacting the outer surface of theproduct 5.

The treatment sleeve 10 having the D-shaped entrance and exit openings,illustrated in FIGS. 1-4, is formed of a plurality of abutting plates 12and 15. As illustrated, there are four channel plates 12 between a pairof face plates 15. A wiper element 14 is positioned between each of theplates 12 and 15. The wiper elements 14 have an opening smaller than theentrance and exit openings, and thus project centrally on each side ofthe interior surfaces 22 of the channel plates 12 to define channels 16.The face plates 15 are provided to secure the wipers 14 to the adjacentchannel plates 12 proximate the entrance and exit openings of thetreatment sleeve 10. As illustrated in FIGS. 3 and 4, each of the plateshas a fluid inlet 18 and a fluid outlet 20. The fluid inlet 18 includesa nozzle 26 aimed to direct the fluid flow around the interior surface22 of the channel 16. The nozzle 26 is in fluid communication with inletplumbing 24 which comprises fluid passages between adjacent plates via anozzle inlet 28. In close proximity to the fluid inlet 18 is the fluidoutlet 20, positioned to allow fluid to exit the channel 16 afterapproximately a single revolution around the interior surfaces 22 of theplate 12. The interior surfaces 22 of the channel 16 adjacent the fluidoutlet 20 include downwardly inclined surfaces 25 directed toward theoutlet 20 to facilitate drainage of any condensate. Similar to the fluidinlet 18, the fluid outlet 20 is in fluid communication with outletplumbing 29 extending between adjacent plates 12 and 15.

The plates 12 are arranged such that the fluid flow in each respectivechannel plate 12 alternates between clockwise and counterclockwise. Forexample, in the first channel plate 12 closest to the entrance openingof the sleeve the fluid flow is in a clockwise direction relative to theexit opening. The next channel plate 12 has a counterclockwise fluidflow, followed by a plate 12 with a clockwise fluid flow, and finally aplate 12 with a counterclockwise fluid flow. The widths of the plates 12and 15 are selected to minimize the amount of space that the treatmentsleeve 10 occupies on the food processing equipment. The plates 12 and15 are each preferably about 0.25 inches in width, resulting in a totallength of the treatment sleeve 10 of about 3 inches.

The treatment sleeve 100 illustrated in FIGS. 7-13 has a pair of helicalflow channels 110 and 120 around its interior. As shown in FIG. 8, thepair of helical flow channels 110 and 120 are configured in a doublehelix arrangement. Each of the helical flow channels 110 and 120 has apair of inlets 122. The two helical flow channels 110 and 120 each sharea common outlet 124. The inlets 122 are positioned proximate themid-section of the treatment sleeve 100 and the outlets 124 arepositioned proximate the entrance and exit openings for each of thehelical channels 110 and 120, as shown in FIG. 9. Fluid is introducedinto the treatment sleeve 100 via the four inlets 122, two for each ofthe helical channels 1,10 and 120, as illustrated in FIGS. 11 and 12.Because the two inlets 122 for each of the helical flow channels 110 and120 are in the mid-section of the treatment sleeve 100, the fluid flowsalong flow paths defined by each channel 110 or 120 both toward theentrance opening and toward the exit opening. At the entrance opening ofthe treatment sleeve 100, both channels 110 and 120 have a common exitthrough the fluid outlet 124, as shown in FIG. 13. At the exit openingof the treatment sleeve 100, a pair of fluid outlets 124 are provided,one for each of the helical flow channels 110 and 120, as illustrated inFIG. 10.

Turning to more of the details of the dual helix treatment sleeve 100,the sleeve 100 is configured for treating product with a diameter ofabout 4.25 inches. The sleeve 100 is between about 9 and 10 inches inlength, and preferably about 9.5 inches; between about 5 and 7 inches inheight, and preferably about 6 inches; and between about 5 and 7 inchesin width, and preferably about 6 inches. The minor radius of theinterior of the multi-directional double helix treatment sleeve 100 isbetween 2 and 2.3 inches, and is preferably about 2.15 inches. The majorradius of the interior of the multi-directional double helix treatmentsleeve 100 is between about 2.25 and 2.55 inches, and is preferablyabout 2.4 inches. Thus, the depth of the channels 110 and 120 ispreferably about 0.25 inches. The helical channels 110 and 120 are eachpreferably at an 80° incline relative to the length direction of thetreatment sleeve 100, and spaced 1.25 inches apart per revolution. Thesedimensions are merely given by way of example, and can be readily scaledup or down, or otherwise varied, in accordance with particular sizingrequirements for different profiles of food products.

Similar to the treatment sleeve 100 of FIGS. 7-13, the treatment sleeve200 of FIGS. 14-17 has a pair of helical flow channels 210 and 211around its interior in a double helix arrangement. Each of the helicalflow channels 210 and 211 has a single fluid inlet 212 or 216 and asingle fluid outlet 214 or 218, as illustrated in FIGS. 15-17. One ofthe flow channels 211 has its inlet 212 positioned proximate theentrance opening and its outlet 218 positioned proximate the exitopening so that fluid is directed from the entrance opening to the exitopening. The other of the flow channels 210 has its outlet 214positioned proximate the entrance opening and its inlet 216 positionedproximate the exit opening so that fluid is directed from the exitopening to the entrance opening. When the fluid is steam, the oppositelydirected flow paths of the fluid in the fluid channels 210 and 211ensures that the steam contacts the surface of the food product 5 soonafter it enters and soon before it exits the treatment sleeve 200 totreat the outer surface, which also can quickly initiate desired flow.Thus, the amount of condensed steam, with reduced heat transferproperties, that may be present at either the entrance or exit openingsof the sleeve 200 can be reduced.

The details of the dual helix treatment 200 sleeve of FIGS. 14-17 aresimilar to the multi-direction dual helix treatment sleeve 100 of FIGS.7-13, except that the sleeve is between about 4.75 and 6.75 inches inlength, and preferably about 5.75 inches. As discussed above, althoughparticular scaled or otherwise modified to accommodate a variety ofdifferent food product profiles.

The treatment sleeve 200 has a wiper element 220 positioned proximateboth the entrance opening and the exit opening, for the purposesdiscussed above in greater detail. The wiper elements 220 are attachedto the treatment sleeve via rings 222, as illustrated in FIG. 14,thereby allowing for easy removal of the wiper elements 220 forreplacement. A lead-in block 202 is attached to the treatment sleeve 200proximate the entrance opening to ensure that the food product 5 isproperly directed into the interior of the sleeve 200. The lead-in block202 has an inclined surface 204 that tapers toward the entrance openingto facilitate alignment of the food product 5 with the interior of thesleeve 200.

The food product 5 is advanced through the treatment sleeves 10, 100 and200 using an advancement mechanism 60. The advancement mechanism 60comprises a longitudinally extending track 40 aligned with alongitudinal axis of the sleeve 10, as illustrated in FIG. 3. Theadvancement mechanism 60 further comprises a pusher device 30 movablerelative to the track 40 for pushing the food product 5 along the track40 and through the treatment sleeve 10. Various driving methods may beused for moving the pusher device 30 relative to the track 40. Forexample, a screw-type drive, pneumatic drive, or a chain or belt drivemay be used for advancing the pusher device 30. The rate at which theadvancement mechanism 60 feeds the food product through the sleeve canbe controlled via a computerized controller. The rate can be determinedupon such factors as the thickness of desired slices when the foodproduct is immediately sliced downstream of the sleeve and the desireddwell time within the sleeve. For example, a seven foot length of foodproduct may be advanced through the sleeve at a rate effective toproduce 2000 slices per minute of the food product when a slicingstation is positioned immediately downstream of the sleeve.

The pusher device 30 includes an arm 32 for movable connection relativeto the drive and the track and a food product-facing pusher portion 44,as illustrated in FIGS. 5A and 5B. When the pusher device 30 is advancedtoward the treatment sleeve 10, the pusher portion 44 contacts an end ofthe food product 5 to push the food product 5 through the sleeve 10. Thedistance between the arm 32 and the pusher portion 44 is preferablyselected to ensure that the pusher portion 44 is able to extendcompletely or at least partially through the steam sleeve 10, 100 or200, as illustrated in FIG. 2, in order to maximize the amount of foodproduct 5 passed through the treatment sleeve 10, 100 or 200.

The pusher portion 44 has a flexible flange member 48 positioned at oneend to securely abut the end of the food product 5 in order to assist inmaintaining a vacuum seal between the end of the food product 5 and thepusher portion 44. The flange member 48 protrudes from the end face ofthe pusher portion 44 and partially surrounds the trailing face of thefood product 5. The flange member is preferably formed of a flexibleplastic or rubber material suitable for contact with food products, andis inserted into a groove formed 148 formed on the face of the pusherportion 44 abutting the food product 5.

The pusher portion 44 also has an aperture 49 connected to a vacuumassembly 46 for further securing the food product 5 to the pusher 30when vacuum is applied. The vacuum assembly 46 comprises a hollow shaft143 having the pusher portion 44 mounted at one end thereof. A gasket145 is positioned between the pusher portion 44 and the hollow shaft 143to reduce pressure losses when a vacuum is applied. The opposite end ofthe hollow shaft 143 is removable received within a bore 149 within amounting block 147, which is secured to the arm 32. The bore 149 extendsthrough the mounting block 147, as shown in FIG. 5B. One end of the bore149 has a diameter sufficient to receive the hollow shaft 143, and agasket 151 is positioned therebetween to reduce pressure losses when avacuum is applied. The other end of the bore 149 has a differentdiameter than the first end, and has a vacuum connection 153 permanentlyreceived therein. A step 155 is located within the bore 149 where thebore changes diameters to provide a stop for fixing the relativeposition between the hollow shaft 143 and the mounting block 147. When avacuum is applied via the vacuum connection 153, the pressure dropcontinues through the bore 149, through the hollow shaft 143, andthrough the aperture 49 formed in the end of the pusher portion 44facing the food product 5. A screen 157 is positioned within theaperture 49 to restrict portions of the food product 5 from entering thehollow shaft 143 when the vacuum is applied. The face of the pusherportion 44 abutting the food product 5 is configured with a pair ofconcentric, raised rings 162 and 164. The rings 162 and 164 each havemultiple notches formed therein. When vacuum is applied to draw the foodproduct 5 against the pusher portion 44, the rings 162 and 164 assist inevenly distributing the vacuum forces along the trailing face of thefood product 5. In particular, the raised rings 162 and 164, along withthe flange member 48, can allow for food products 5 having variations inthe trailing face surface to be securely maintained against the pusherportion 44 when a vacuum is applied.

The pusher portion 44 may be sized and shaped to closely fit within theopening of the wiper elements 14 in order to assist in maintaining thedesired flow characteristics of the fluid as the pusher portion 44 urgesthe food product 5 through the steam sleeve 10, 100 or 200. For example,if the food product has a D-shaped profile, the pusher portion may havea corresponding D-shaped profile. The pusher portion 44 is attached tothe pusher 30 via threads, so that the pusher portions can be easilyinterchanged and cleaned.

The pusher portion 44, along with the hollow shaft 143, are configuredto be removable from the mounting block 147 in order to allow forcleaning and replacement with pusher portions 44 having different sizesand profiles. A protruding securement element 161 is attached to theshaft 143, as shown in FIGS. 5A and 5B. The securement element 161 has anotch 165 for receiving a free end of a clamp 167. An end of the clamp167 opposite the free end is secured to a clamp actuator 163. The clampactuator 163 is movable between a disengaged position allowing for thefree end of the clamp 167 to be removable from and insertable into thenotch 165 of the securement element 161 and an engaged position securingthe clamp 167 in the notch 165 of the securement element 161 to securethe pusher portion 44 and shaft 143 relative to the mounting block 147.

The steam sleeve 10, 100, 200 may be used in a commercial foodprocessing operation 300. The commercial food processing operation mayproceed through multiple treatment areas, as depicted in FIG. 6. Thetreatment areas where the food product is subjected to differenttreatments can include a cooking zone 302, a water deluge zone 304, awater submergence zone 306, a chilling zone 308, an equilibration zone310, and a slicing and packaging zone 312. The sleeve 10, 100 or 200 ispreferably used after the chill zone 308 and prior to the equilibrationzone 310. The sleeve is also preferably used prior to the slicing andpackaging zone 312. However, the sleeve 10, 100 or 200 can be usedbetween or as part of other operations.

Various other equipment can be used with the sleeve 10, 100 or 200during the food processing operation 300. For example, a steam hood 314can be positioned adjacent the sleeve 10, 100 or 200 in order to removeexcess steam and/or condensate proximate the exterior of the sleeve 10,100 or 200, as depicted in FIG. 19. The removal of excess steam and/orcondensate can desirably reduce moisture levels which can contribute tomicrobial activity in the environment proximate the sleeve 10, 100 or200.

A slide gate 316 may be provided at one or both of the entrance and exitopenings of the sleeve 10, 100 or 200 in order to prevent the escape ofsteam prior to the food product 5 being fed adjacent to the gate 316. Tothis end, the gate 316 is configured to seal the exit opening,downstream of the entrance opening and in the feed direction, of thesleeve 10, 100 or 200 when in a closed position. The gate 316 isshiftable to an open position, such as when the food product is spanningthe interior of the sleeve 10, 100 of 200 between the entrance and exitopenings thereof, allowing passage of the food product 5 through thesleeve 10, 100 or 200. The gate 316 preferably is formed of a plastic,and may be an ultrahigh molecular weight plastic such as DELRIN®. Thegate 316 may be slid along pins projecting from the downstream end ofthe sleeve, and may be controlled by a motor or an air cylinder.

The use of the gate 316 also allows for the sleeve 10, 100 or 200 to beused for treating the leading end face of the food product 5, such aswhen the food product is initially being fed through the entranceopening of the steam sleeve and the gate 316 is in its closed position,thereby allowing for steam to leave the channels and contact the leadingend face of the food product 5. The trailing end face of the foodproduct can be treated by stopping the forward movement of the foodproduct 5 just before the trailing face exits the sleeve, and thenretracting the pusher portion 44 to briefly treat the pusher portion 44face and the trailing end face of the food product 5. After treatment ofthe trailing end face of the food product 5, the trailing end face canbe advanced out of the sleeve 10, 100, or 200.

When used prior to a slicing zone 314, the steam sleeve 10, 100 or 200is preferably placed immediately adjacent the slicing apparatus 318, asillustrated in FIG. 19, in order to minimize spacing between the exitopening of the sleeve 10, 100 or 200 and the slicing apparatus and thusminimize exposure of the food product 5 prior to slicing.

As will be appreciated, methods and apparatus for treating a surface ofa food product are provided using a fluid having properties selected fortreating the surface and bringing the fluid into contact with an outersurface of the food product in a generally continuous manner in acommercial food processing environment. The invention is not limited tothe embodiments described hereinabove or to any particular embodiments.For example, various modifications to the number, direction, and size ofthe flow channels will result in substantially the same invention.

The invention is defined more particularly by the following claims:

1-16. (canceled)
 17. An apparatus for treating the surface of a foodproduct with fluid, the apparatus comprising: a sleeve having anentrance opening and an exit opening, the entrance and exit openingsbeing sized approximately the same as a cross-sectional profile of thefood product; a plurality of channels formed in an interior of thesleeve between the entrance opening and the exit opening, the channelscapable of directing the flow of fluid at least partially around anouter portion of the food product, and at least one of the channelshaving a fluid inlet and at least one of the channels having a fluidoutlet to permit the introduction and removal of the fluid into thesleeve.
 18. An apparatus in accordance with claim 17, wherein at leastsome of the plurality of channels are connected in a generally helicalarrangement providing a continuous fluid flow path from the fluid inletto the fluid outlet.
 19. An apparatus in accordance with claim 18,wherein at least two generally helical arrangements of the plurality ofchannels are provided forming two separate continuous fluid flow pathsfrom fluid inlets to fluid outlets.
 20. An apparatus in accordance withclaim 17, wherein a seal element is provided proximate at least one ofthe sleeve entrance and exit openings, the seal element having anopening substantially the same size as the cross-sectional profile ofthe food product and smaller than the opening of the at least one of thesleeve entrance and exit openings.
 21. An apparatus in accordance withclaim 20, wherein the entrance opening and exit opening have a shapegenerally the same as the seal element opening shape.
 22. An apparatusin accordance with claim 20, wherein the entrance opening, exit opening,and seal element openings are all either circular, D-shaped,rectangular, oval or square.
 23. An apparatus in accordance with claim17, wherein the sleeve is formed of a plurality of plates arranged in anadjacent manner, the plates each having an opening therethrough and oneof the plurality of channels formed adjacent the opening in an interiorof the plate, the channels each having an inlet and an outlet andgenerally surrounding the plate opening.
 24. An apparatus in accordancewith claim 23, wherein the channel inlets and outlets of adjacent platesare staggered to define flow paths in adjacent plates having alternatingdirections.
 25. An apparatus in accordance with claim 23, wherein sealelements are positioned between adjacent plates and at least partiallydefine the channels.
 26. An apparatus for treating an outer surface of afood product, the apparatus comprising: means for generating a flow ofsteam in an interior of a steam sleeve having an entrance and an exit,the steam having selected properties to treat the outer surface of thefood product; and means for advancing a food product having an outersurface in a feed direction through the interior of the steam sleevebetween the entrance and exit thereof, the flow of steam in the steamsleeve contacting the outer surface of the food product while the foodproduct is passing therethrough at the predetermined temperature fortreating the outer surface of the food product.
 27. An apparatus fortreating an outer surface of a food product in accordance with claim 26,including means for directing steam condensation away from the outersurface of the food product.